JP2003117367A - Gas mixer - Google Patents
Gas mixerInfo
- Publication number
- JP2003117367A JP2003117367A JP2001320547A JP2001320547A JP2003117367A JP 2003117367 A JP2003117367 A JP 2003117367A JP 2001320547 A JP2001320547 A JP 2001320547A JP 2001320547 A JP2001320547 A JP 2001320547A JP 2003117367 A JP2003117367 A JP 2003117367A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- blower
- air
- elbow
- pipe
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 14
- 230000003247 decreasing effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 157
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 123
- 238000010586 diagram Methods 0.000 description 16
- 229910021529 ammonia Inorganic materials 0.000 description 15
- 238000010790 dilution Methods 0.000 description 15
- 239000012895 dilution Substances 0.000 description 15
- 239000006185 dispersion Substances 0.000 description 7
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 238000007865 diluting Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 230000003014 reinforcing effect Effects 0.000 description 2
- 239000003054 catalyst Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、空気に他のガス、
例えばアンモニアガスを低濃度に混合させるガス混合器
に関する。TECHNICAL FIELD The present invention relates to air, other gases,
For example, it relates to a gas mixer for mixing ammonia gas at a low concentration.
【0002】[0002]
【従来の技術】図8に基づき、従来の空気に他のガスを
低濃度に混合させるガス混合器の例として、ボイラ排ガ
ス中の窒素酸化物を除去する脱硝装置に供給される空気
とアンモニアガスの混合ガスを得るために、空気にアン
モニアを低濃度に混合するガス混合器の系統図を示す。2. Description of the Related Art Referring to FIG. 8, as an example of a conventional gas mixer for mixing another gas with a low concentration, air and ammonia gas supplied to a denitration device for removing nitrogen oxides from boiler exhaust gas 3 is a system diagram of a gas mixer that mixes ammonia with air at a low concentration to obtain the mixed gas of FIG.
【0003】図8において、送風機1には送風機出口配
管2が接続されて送風機1から空気が送入され、送風機
出口配管2の途中にはアンモニアガス供給管3がその出
口開口31を送風機出口配管2の上流に向けて差し込ま
れて設置されている。アンモニアガス供給管3の上流側
には図示しないアンモニアガス供給装置が接続してい
る。In FIG. 8, a blower outlet pipe 2 is connected to the blower 1 so that air is blown from the blower 1, and in the middle of the blower outlet pipe 2, an ammonia gas supply pipe 3 has its outlet opening 31 through the blower outlet pipe. It is inserted and installed toward the upstream of 2. An ammonia gas supply device (not shown) is connected to the upstream side of the ammonia gas supply pipe 3.
【0004】送風機出口配管2のアンモニアガス供給管
3が設置された位置より下流側には配管直径Dの約20
倍の長さL(L=約20D)の直管部4が接続され、直
管部4は脱硝装置のダクト5内の複数のアンモニアガス
注入ノズル6へ分れて接続している。About 20 pipe diameters D are provided downstream of the position where the ammonia gas supply pipe 3 of the blower outlet pipe 2 is installed.
A straight pipe part 4 having a double length L (L = about 20 D) is connected, and the straight pipe part 4 is divided and connected to a plurality of ammonia gas injection nozzles 6 in a duct 5 of the denitration device.
【0005】上記のようなアンモニアガス供給管3と直
管部4で構成される従来のガス混合器10においては、
送風機1より送入された空気aは送風機出口配管2を通
り、送風機出口配管2の途中に設置されたアンモニアガ
ス供給管3から送風機出口配管2内に空気流れ方向と逆
向きに100%濃度のアンモニアガスbが送入され、直
管部4で100%濃度のアンモニアガスbは空気aと混
合し希釈され、低濃度のアンモニア混合ガスcとなっ
て、下流側に接続する脱硝装置のダクト5内のアンモニ
アガス注入ノズル6へ分配供給され、ダクト5内を流れ
る排ガスg内に噴出されるようになっている。In the conventional gas mixer 10 composed of the ammonia gas supply pipe 3 and the straight pipe portion 4 as described above,
The air a blown from the blower 1 passes through the blower outlet pipe 2 and from the ammonia gas supply pipe 3 installed in the blower outlet pipe 2 into the blower outlet pipe 2 in the direction opposite to the air flow direction with 100% concentration. Ammonia gas b is fed in, and 100% concentration ammonia gas b is mixed with air a in the straight pipe portion 4 to be diluted to become low concentration ammonia mixed gas c, which is a duct 5 of the denitration device connected to the downstream side. It is distributed and supplied to the ammonia gas injection nozzle 6 inside and is ejected into the exhaust gas g flowing in the duct 5.
【0006】[0006]
【発明が解決しようとする課題】しかし、上述した従来
のガス混合器10には以下の問題があった。すなわち、
脱硝装置において排ガスg中の窒素酸化物が触媒層で除
去されるためには、送風機1から送入される空気aで1
00%濃度のアンモニアガスbを低濃度に希釈しアンモ
ニア混合ガスcのアンモニア濃度のばらつきを1%以内
に収めて、脱硝装置のダクト5内のアンモニア注入ノズ
ル6へ分配し、排ガスg中に供給する必要がある。10
0%濃度のアンモニアガスbが空気aで低濃度に希釈さ
れ、アンモニア濃度のばらつきを1%以内に収めるには
直管部4の長さを長くとることが必要であるが、直管部
4が長くなると配管製作コストが上がり、配管を配置す
るスペースにも制約があるなどのデメリットがある。However, the conventional gas mixer 10 described above has the following problems. That is,
In the denitration device, in order to remove the nitrogen oxides in the exhaust gas g in the catalyst layer, the air a fed from the blower 1
Ammonia gas b with a concentration of 00% is diluted to a low concentration so that the dispersion of the ammonia concentration of the ammonia mixed gas c is kept within 1%, and it is distributed to the ammonia injection nozzle 6 in the duct 5 of the denitration device and supplied into the exhaust gas g. There is a need to. 10
The 0% concentration of ammonia gas b is diluted with air a to a low concentration, and it is necessary to increase the length of the straight pipe portion 4 in order to keep the variation in the ammonia concentration within 1%. If the length is too long, there will be disadvantages such as higher pipe manufacturing costs and restrictions on the space for arranging the pipes.
【0007】本発明は、空気aにアンモニアガスbを低
濃度に混合希釈でき、アンモニア濃度のばらつきを微小
に、例えば1%程度以内に収まるような混合性能を備
え、配管スペースがコンパクトなガス混合器を提供する
ことを課題とするものである。The present invention can mix and dilute the ammonia gas b into the air a to a low concentration and has a mixing performance such that the dispersion of the ammonia concentration is small, for example, within about 1%, and the piping space is compact. It is an object to provide a container.
【0008】[0008]
【課題を解決するための手段】(1)本発明は上記の課
題を解決するためになされたものであって、その第1の
手段として、送風機に接続され同送風機から空気が送入
される送風機出口配管、同送風機出口配管内にガス出口
開口を前記空気の流れの上流側に向け差し込まれて設置
され、同ガス出口開口からガスを前記送風機出口配管内
に送入するガス供給管、同送風機出口配管に前記ガス供
給管の位置より下流側で接続するエルボ、同エルボの下
流側に接続する直管部を有してなることを特徴とするガ
ス混合器を提供する。Means for Solving the Problems (1) The present invention has been made to solve the above problems, and as a first means thereof, is connected to a blower and air is blown from the blower. A blower outlet pipe, a gas outlet opening is installed in the blower outlet pipe toward the upstream side of the air flow, and a gas supply pipe for feeding gas from the gas outlet opening into the blower outlet pipe, There is provided a gas mixer characterized by having an elbow connected to a blower outlet pipe at a downstream side of a position of the gas supply pipe and a straight pipe portion connected to a downstream side of the elbow.
【0009】上記の構成により、第1の手段のガス混合
器によれば、ガス供給管から、ガスが空気の流れと逆向
きに送入されるとガスは空気の流れに追従されず混合が
促進され希釈されやすくなるが、さらに、空気の流れが
エルボの曲がりの内縁部で剥離を発生し逆流域が生じ、
空気が乱されることにより、ガスの混合が促進され、短
い直管部でも希釈されやすくなり、大量の空気と微量の
高濃度のガスを濃度のばらつきを微小に、例えば1%以
内に収めて低濃度に混合希釈できる。According to the gas mixer of the first means having the above structure, when the gas is introduced from the gas supply pipe in the direction opposite to the air flow, the gas does not follow the air flow and is mixed. Although it is promoted and easily diluted, the flow of air causes separation at the inner edge of the bend of the elbow, creating a backflow region,
When the air is disturbed, mixing of the gas is promoted, and even a short straight pipe portion is likely to be diluted, and a large amount of air and a small amount of a high concentration gas have a small concentration variation, for example, within 1%. Can be mixed and diluted to a low concentration.
【0010】(2)第2の手段としては、第1の手段の
ガス混合器において、前記直管部の入口部内部に同直管
部の中心軸回りにひねって形成されたひねり板を取り付
けてなることを特徴とするガス混合器を提供する。(2) As a second means, in the gas mixer of the first means, a twist plate formed by twisting around the central axis of the straight pipe portion is attached inside the inlet portion of the straight pipe portion. A gas mixer is provided.
【0011】第2の手段のガス混合器によれば、第1の
手段のガス混合器の作用に加え、空気とガスがひねり板
に沿って流れ、旋回流が発生し混合希釈を促進し、ガス
が短い直管部で十分希釈され、大量の空気と微量の高濃
度のガスを濃度のばらつきを微小に、例えば1%以内に
収めて低濃度に混合希釈できる。According to the gas mixer of the second means, in addition to the function of the gas mixer of the first means, air and gas flow along the twist plate to generate a swirling flow to promote mixing and dilution, The gas is sufficiently diluted in a short straight pipe portion, and a large amount of air and a small amount of high-concentration gas can be mixed and diluted to a low concentration with a minute variation in concentration, for example, within 1%.
【0012】(3)また、第3の手段として、第1の手
段のガス混合器において、前記直管部の入口部内部にオ
リフィスを備えてなることを特徴とするガス混合器を提
供する。(3) As a third means, there is provided a gas mixer according to the first means, characterized in that an orifice is provided inside the inlet portion of the straight pipe portion.
【0013】第3の手段のガス混合器によれば、第1の
手段のガス混合器の作用に加え、直管部の入口部にオリ
フィスを設置することでオリフィスの絞りにより一旦流
れがせき止められガスの混合希釈を促進し、ガスが短い
直管部でも希釈されやすくなり、大量の空気と微量の高
濃度のガスを濃度のばらつきを微小に、例えば1%以内
に収めて低濃度に混合希釈できる。According to the gas mixer of the third means, in addition to the function of the gas mixer of the first means, by installing an orifice at the inlet of the straight pipe portion, the flow is once stopped by the restriction of the orifice. It promotes the mixing and dilution of the gas, making it easier for the gas to be diluted even in a short straight pipe section, and mixing and diluting a large amount of air and a small amount of a high concentration gas to a low concentration by keeping the variation in concentration to a minute, for example, within 1%. it can.
【0014】(4)第4の手段として、第3の手段のガ
ス混合器において、前記送風機出口配管内に前記ガス出
口開口に対面して取り付けられた衝突板を備えてなるこ
とを特徴とするガス混合器を提供する。(4) As a fourth means, in the gas mixer of the third means, a collision plate is provided in the blower outlet pipe so as to face the gas outlet opening. Provide a gas mixer.
【0015】第4の手段のガス混合器によれば、第3の
手段のガス混合器の作用に加え、送風機からの空気は送
風機出口配管途中の衝突板に衝突し、衝突板外周に広が
り流れた空気は衝突板で剥離して乱れ、ガス供給管より
送入されたガスは衝突板への衝突により衝突板外周に広
がり、乱れた空気の流れにより希釈されやすくなり、大
量の空気と微量の高濃度のガスを濃度のばらつきを微小
に、例えば1%以内に収めて低濃度に混合希釈できる。According to the gas mixer of the fourth means, in addition to the function of the gas mixer of the third means, the air from the blower collides with a collision plate in the middle of the blower outlet pipe and spreads to the outer periphery of the collision plate. The separated air is separated and disturbed by the collision plate, and the gas introduced from the gas supply pipe spreads to the outer periphery of the collision plate due to the collision with the collision plate, and is easily diluted by the disturbed air flow. It is possible to mix and dilute a high-concentration gas into a low-concentration while keeping the variation in the concentration very small, for example, within 1%.
【0016】(5)第5の手段として、送風機に接続さ
れ同送風機から空気が送入される送風機出口配管、同送
風機出口配管の下流側に接続するエルボ、同エルボの下
流側に接続する直管部、前記エルボの曲がりの内縁部の
直後にガス出口開口が開口するように設置され、同ガス
出口開口からガスを前記エルボ内に送入するガス供給管
を有してなることを特徴とするガス混合器を提供する。(5) As a fifth means, a blower outlet pipe connected to the blower and into which air is sent from the blower, an elbow connected to the downstream side of the blower outlet pipe, and a direct connection to the downstream side of the elbow. A pipe part, which is installed so that a gas outlet opening opens immediately after the inner edge of the bend of the elbow, and has a gas supply pipe for feeding gas into the elbow from the gas outlet opening. A gas mixer is provided.
【0017】第5の手段のガス混合器によれば、送風機
より送入される空気はエルボの曲がりの内縁部で剥離
し、逆流域が比較的広範囲で生じ、逆流域に投入された
ガスは逆流域で対流しながら徐々に空気と混合し、さら
に直管部で希釈されるので、多量の空気と微量の高濃度
のガスを濃度のばらつきを微小に、例えば1%以内に収
めて低濃度に混合希釈できる。According to the gas mixer of the fifth means, the air blown from the blower is separated at the inner edge of the bend of the elbow, a backflow region is generated in a relatively wide range, and the gas injected into the backflow region is It gradually mixes with air while convection in the reverse flow area, and is further diluted in the straight pipe section, so a large amount of air and a small amount of high concentration gas can be contained in a small concentration variation, for example, within 1%, to achieve low concentration. Can be mixed and diluted.
【0018】(6)第6の手段として、送風機に接続さ
れ同送風機から空気が送入される送風機出口配管、同送
風機出口配管の下流側に接続するエルボ、同エルボの下
流側に接続する直管部、同直管部の入口部内部に形成さ
れたディフューザ、同ディフューザの絞り部の外周に備
えられたリングヘッダ、同リングヘッダに連通して設置
されたガス供給管、同リングヘッダに前記絞り部の中心
に向け突設され前記ガス供給管から供給されたガスを前
記絞り部内に送入する複数のノズルを有してなることを
特徴とするガス混合器を提供する。(6) As a sixth means, a blower outlet pipe connected to the blower and into which air is sent from the blower, an elbow connected to the downstream side of the blower outlet pipe, and a direct connection to the downstream side of the elbow. The pipe part, the diffuser formed inside the inlet part of the straight pipe part, the ring header provided on the outer periphery of the throttle part of the diffuser, the gas supply pipe installed in communication with the ring header, and the ring header There is provided a gas mixer characterized by comprising a plurality of nozzles projecting toward the center of a narrowed portion and feeding gas supplied from the gas supply pipe into the narrowed portion.
【0019】第6の手段のガス混合器によれば、送風機
より送入される空気はディフューザの絞り部で縮流さ
れ、ガス供給管を介してリングヘッダに供給されたガス
はノズルから絞り部の中心近くに送入され空気の縮流と
混合し、希釈されやすくなり、短い直管部で多量の空気
と微量の高濃度のガスを濃度のばらつきを微小に、例え
ば1%以内に収めて低濃度に混合希釈できる。According to the gas mixer of the sixth means, the air fed from the blower is contracted by the throttle of the diffuser, and the gas supplied to the ring header through the gas supply pipe is throttled by the nozzle. It is sent near the center of the air and mixes with a contracted flow of air, which makes it easy to dilute it. With a short straight pipe part, a large amount of air and a small amount of high-concentration gas can be stored with a slight variation in concentration, for example, within 1%. Can be mixed and diluted to a low concentration.
【0020】(7)第7の手段として、送風機に接続さ
れ同送風機から空気が送入される送風機出口配管、同送
風機出口配管の下流側に接続するエルボ、同エルボの下
流側に接続する直管部、同エルボ内の下流側において前
記空気の流れの下流方向に向いて前記直管部内に延在す
るように差し込まれて設置されガス出口開口が同空気の
流れの下流方向に向けて開口し同ガス出口開口から前記
直管部内にガスを送入するガス供給管、同ガス供給管の
外周に取り付けられた螺旋状のフィンを有してなること
を特徴とするガス混合器を提供する。(7) As a seventh means, a blower outlet pipe connected to the blower and into which air is introduced, an elbow connected to the downstream side of the blower outlet pipe, and a direct connection to the downstream side of the elbow. On the downstream side of the pipe part and the elbow, the gas outlet opening is installed so as to extend in the straight pipe part toward the downstream direction of the air flow, and the gas outlet opening is opened toward the downstream direction of the air flow. A gas mixer characterized by having a gas supply pipe for feeding gas into the straight pipe portion from the gas outlet opening, and a spiral fin attached to the outer periphery of the gas supply pipe. .
【0021】第7の手段のガス混合器によれば、送風機
より送入された空気は、ガス供給管の外周の螺旋状のフ
ィンに沿って流れ、発生した旋回流中にガス供給管から
送入されたガスが空気と混合希釈されやすくなり、短い
直管部で多量の空気と微量の高濃度のガスを濃度のばら
つきを微小に、例えば1%以内に収めて低濃度に混合希
釈できる。According to the gas mixer of the seventh means, the air sent from the blower flows along the spiral fins on the outer circumference of the gas supply pipe and is sent from the gas supply pipe into the generated swirling flow. The introduced gas is likely to be mixed and diluted with air, and a large amount of air and a small amount of high-concentration gas can be mixed and diluted to a low concentration with a small concentration variation, for example, within 1%, in a short straight pipe portion.
【0022】[0022]
【発明の実施の形態】図1に基づき、本発明の実施の第
1形態にかかるガス混合器を説明する。図1は本実施の
形態のガス混合器11の系統図である。図1において、
従来例と同様の部分については同じ符号を付して、説明
を省略し、異なる部分を主に説明する。BEST MODE FOR CARRYING OUT THE INVENTION A gas mixer according to a first embodiment of the present invention will be described with reference to FIG. FIG. 1 is a system diagram of a gas mixer 11 of this embodiment. In FIG.
The same parts as those of the conventional example are designated by the same reference numerals, the description thereof will be omitted, and different parts will be mainly described.
【0023】図1に示すように、送風機1には送風機出
口配管2が接続されて送風機1から空気aが送入され、
送風機出口配管2の途中には空気aの流れと逆向きにア
ンモニアガス供給管3がその出口開口31を送風機出口
配管2の上流に向けて差し込まれて設置されている。As shown in FIG. 1, a blower outlet pipe 2 is connected to the blower 1 so that air a is fed from the blower 1,
An ammonia gas supply pipe 3 is installed in the middle of the blower outlet pipe 2 in a direction opposite to the flow of the air a, with its outlet opening 31 inserted toward the upstream side of the blower outlet pipe 2.
【0024】なお、アンモニアガス供給管3の上流側に
は図示しないアンモニアガス供給装置が接続している
が、後述の他の実施の形態においてその点は同様である
ので繰り返し説明することは省略する。An ammonia gas supply device (not shown) is connected to the upstream side of the ammonia gas supply pipe 3, but this point is the same in other embodiments to be described later, and repeated description will be omitted. .
【0025】アンモニアガス供給管3の設置された位置
の下流側の送風機出口配管2にはエルボ7が接続され、
エルボ7の下流側には直管部4が接続されている。An elbow 7 is connected to the blower outlet pipe 2 on the downstream side of the position where the ammonia gas supply pipe 3 is installed,
The straight pipe portion 4 is connected to the downstream side of the elbow 7.
【0026】上記のようなアンモニアガス供給管3とエ
ルボ7と直管部4で構成される本実施の形態のガス混合
器11においては、送風機出口配管2内に空気aの流れ
と逆向きに出口開口31を向けて設置されたアンモニア
ガス供給管3から、100%濃度のアンモニアガスbが
空気aの流れと逆向きに送入されると空気aの流れに追
従されず混合が促進され希釈されやすくなるが、本実施
の形態ではさらに、空気aの流れがエルボ7の曲がりの
内縁部で剥離を発生し逆流域8が生じる。このエルボ7
内の逆流域8により空気aが乱されることにより、10
0%濃度のアンモニアガスbの混合が促進され、短い直
管部4でも希釈されやすくなる。In the gas mixer 11 of the present embodiment, which is composed of the ammonia gas supply pipe 3, the elbow 7 and the straight pipe portion 4 as described above, the flow direction of the air a is reversed in the blower outlet pipe 2. When the ammonia gas b having a concentration of 100% is fed in the direction opposite to the flow of the air a from the ammonia gas supply pipe 3 installed with the outlet opening 31 facing, the flow of the air a is not followed and the mixing is promoted and the dilution is performed. However, in the present embodiment, the flow of the air a further causes separation at the inner edge of the bend of the elbow 7 and the backflow region 8 is generated. This elbow 7
When the air a is disturbed by the backflow region 8 inside,
Mixing of the 0% concentration ammonia gas b is promoted, and even the short straight pipe portion 4 is easily diluted.
【0027】したがって、100%濃度のアンモニアガ
スbを空気aの流れと逆向きに送入し、さらに下流側に
エルボ7を設置することにより、短い直管部4で大量の
空気aと微量の100%濃度のアンモニアガスbをアン
モニア濃度のばらつきを微小に、例えば1%以内に収め
て低濃度に混合希釈でき、直管部4が従来の半分以下で
すみコストの低減を図ることができる。Therefore, by supplying 100% -concentration ammonia gas b in the direction opposite to the flow of the air a, and further installing the elbow 7 on the downstream side, a large amount of air a and a small amount of air a can be obtained in the short straight pipe section 4. A 100% concentration of ammonia gas b can be mixed and diluted to a low concentration with a slight variation in the ammonia concentration, for example, within 1%, and the straight pipe portion 4 can be reduced to less than half of the conventional cost, and the cost can be reduced.
【0028】図2に基づき、本発明の実施の第2形態に
かかるガス混合器を説明する。図2(a)は本実施の形
態のガス混合器12の系統図であり、同図(b)は
(a)中A部拡大断面図である。図2において、従来例
および前述の実施の形態と同様の部分については同じ符
号を付して、説明を省略し、異なる部分を主に説明す
る。なおこのことは、後述の他の実施の形態の説明にお
いて同様とする。A gas mixer according to a second embodiment of the present invention will be described with reference to FIG. FIG. 2A is a system diagram of the gas mixer 12 according to the present embodiment, and FIG. 2B is an enlarged cross-sectional view of a portion A in FIG. In FIG. 2, the same parts as those in the conventional example and the above-described embodiment are designated by the same reference numerals, the description thereof will be omitted, and different parts will be mainly described. Note that this is the same in the description of other embodiments described later.
【0029】図2に示すように、送風機1には送風機出
口配管2が接続されて空気aが送入され、送風機出口配
管2の途中には空気aの流れと逆向きにアンモニアガス
供給管3がその出口開口31を送風機出口配管2の上流
に向けて差し込まれて設置されている。As shown in FIG. 2, a blower outlet pipe 2 is connected to the blower 1 to blow air a therein, and an ammonia gas supply pipe 3 is provided in the middle of the blower outlet pipe 2 in a direction opposite to the flow of the air a. Is installed by inserting the outlet opening 31 toward the upstream side of the blower outlet pipe 2.
【0030】アンモニアガス供給管3の位置の下流側に
はエルボ7が接続され、エルボ7の下流側には、直管部
4の入口部内部に、板を直管部4の中心軸回りに180
°ひねったひねり板26が取り付けられている。An elbow 7 is connected to the downstream side of the position of the ammonia gas supply pipe 3, and on the downstream side of the elbow 7, a plate is provided inside the inlet portion of the straight pipe portion 4 around the central axis of the straight pipe portion 4. 180
° A twist plate 26 is attached.
【0031】上記のようなアンモニアガス供給管3、エ
ルボ7、ひねり板26と直管部4で構成される本実施の
形態のガス混合器12においては、送風機出口配管2途
中に空気aの流れと逆向きに設置されたアンモニアガス
供給管3から、100%濃度のアンモニアガスbが空気
aの流れと逆向きに送入されると空気aの流れに追従さ
れず混合が促進され希釈されやすくなり、また実施の第
1形態で説明したと同様にエルボ7での空気aの逆流域
での混合が行なわれるが、本実施の形態ではさらに、直
管部4入口に配管中心軸周りに180°ひねったひねり
板26を設置することで空気aとアンモニアガスbがひ
ねり板26に沿って流れ、旋回流が発生し混合希釈を促
進し、アンモニアガスbが短い直管部4で十分希釈され
る。In the gas mixer 12 of the present embodiment which is composed of the ammonia gas supply pipe 3, the elbow 7, the twist plate 26 and the straight pipe portion 4 as described above, the flow of the air a in the blower outlet pipe 2 When the ammonia gas b of 100% concentration is sent in the opposite direction to the flow of the air a from the ammonia gas supply pipe 3 installed in the opposite direction, the flow of the air a is not followed and the mixing is promoted and the dilution is likely to occur. In addition, mixing of the air a in the backflow region of the elbow 7 is performed in the same manner as described in the first embodiment, but in the present embodiment, it is further added to the inlet of the straight pipe portion 4 about 180 ° around the pipe central axis. By installing the twisted twisted plate 26, the air a and the ammonia gas b flow along the twisted plate 26, a swirl flow is generated to promote mixed dilution, and the ammonia gas b is sufficiently diluted in the short straight pipe section 4. It
【0032】なお、ひねり板26のひねり角度は180
°に限定されず適宜でよいが、圧損と混合希釈性能のバ
ランスから180°程度が好ましい。The twist angle of the twist plate 26 is 180.
The angle is not limited to 50 °, but may be appropriately set, but is preferably about 180 ° from the viewpoint of balance between pressure loss and mixed dilution performance.
【0033】したがって、100%濃度のアンモニアガ
スbを空気aの流れと逆向きに送入し、エルボ7を設
け、さらにエルボ7下流の直管部4入口に180°ひね
り板を設置することで、短い直管部4で大量の空気aと
微量の100%濃度のアンモニアガスbをアンモニア濃
度のばらつきを微小に、例えば1%以内に収めて低濃度
に混合希釈でき、直管部4が従来の半分以下ですみコス
トの低減を図ることができる。Therefore, by supplying 100% -concentration ammonia gas b in the direction opposite to the flow of the air a, providing the elbow 7, and further installing a 180 ° twist plate at the inlet of the straight pipe section 4 downstream of the elbow 7. In the short straight pipe part 4, a large amount of air a and a very small amount of 100% concentration ammonia gas b can be mixed and diluted to a low concentration by keeping the dispersion of the ammonia concentration small, for example, within 1%. The cost can be reduced by less than half.
【0034】図3に基づき、本発明の実施の第3形態に
かかるガス混合器を説明する。図3は本実施の形態のガ
ス混合器13の系統図である。A gas mixer according to a third embodiment of the present invention will be described with reference to FIG. FIG. 3 is a system diagram of the gas mixer 13 of this embodiment.
【0035】図3に示すように、送風機1には送風機出
口配管2が接続されて空気aが送入され、送風機出口配
管2の途中には空気aの流れと逆向きにアンモニアガス
供給管3がその出口開口31を送風機出口配管2の上流
に向けて差し込まれて設置されている。As shown in FIG. 3, a blower 1 is connected to a blower outlet pipe 2 to blow air a therein, and an ammonia gas supply pipe 3 is provided in the middle of the blower outlet pipe 2 in a direction opposite to the flow of the air a. Is installed by inserting the outlet opening 31 toward the upstream side of the blower outlet pipe 2.
【0036】アンモニアガス供給管3の位置の下流側に
はエルボ7が接続され、エルボ7の下流側には直管部4
が接続されている。そして、エルボ7の下流側の直管部
4の入口部内部に2枚のオリフィス9a、9bが一定間
隔で設置されている。An elbow 7 is connected to the downstream side of the position of the ammonia gas supply pipe 3, and a straight pipe portion 4 is connected to the downstream side of the elbow 7.
Are connected. Then, two orifices 9a and 9b are installed at regular intervals inside the inlet of the straight pipe portion 4 on the downstream side of the elbow 7.
【0037】上記のようなアンモニアガス供給管3、エ
ルボ7、オリフィス9a、9bと直管部4で構成される
本実施の形態のガス混合器13においては、送風機出口
配管2途中に空気aの流れと逆向きに設置されたアンモ
ニアガス供給管3から、100%濃度のアンモニアガス
bが空気aの流れと逆向きに送入されると空気aの流れ
に追従されず混合が促進され希釈されやすくなり、エル
ボ7で発生する空気aの逆流域によっても混合が促進さ
れるが、本実施の形態ではさらに、直管部4の入口部に
オリフィス9a、9bを設置することで1段目のオリフ
ィス9aの絞りにより一旦流れがせき止められアンモニ
アガスbの混合希釈を促進し、更に2段目のオリフィス
9bでも同様に流れがせき止められ混合希釈を促進し、
アンモニアガスbが、短い直管部4でも希釈されやすく
なる。In the gas mixer 13 of the present embodiment, which is composed of the ammonia gas supply pipe 3, the elbow 7, the orifices 9a and 9b, and the straight pipe portion 4 as described above, the air a is provided in the middle of the blower outlet pipe 2. When the ammonia gas b having a concentration of 100% is sent in the opposite direction to the flow of the air a from the ammonia gas supply pipe 3 installed in the opposite direction to the flow, the flow of the air a is not followed and the mixing is promoted and diluted. Although it becomes easier and mixing is promoted also by the backflow region of the air a generated in the elbow 7, in the present embodiment, by further installing the orifices 9a and 9b at the inlet of the straight pipe portion 4, the first stage is provided. By restricting the orifice 9a, the flow is once stopped to promote the mixed dilution of the ammonia gas b, and the second stage orifice 9b also similarly stops the flow to promote the mixed dilution.
The ammonia gas b is likely to be diluted even in the short straight pipe section 4.
【0038】なお、オリフィスは1枚でもよく、また、
複数枚入れる方が混合希釈性能が向上するが、ガス混合
器13中の圧力損失が増大し送風機1等の負荷増大を起
こすおそれがあるので、混合希釈性能とのバランスから
オリフィス枚数は2枚が好ましい。The number of orifices may be one, and
The mixing and diluting performance is improved by inserting a plurality of sheets, but the pressure loss in the gas mixer 13 may be increased and the load of the blower 1 or the like may be increased. Therefore, from the balance with the mixing and diluting performance, two orifices are required. preferable.
【0039】したがって、100%濃度のアンモニアガ
スbを空気aの流れと逆向きに送入し、さらに下流側に
エルボ7を設置し、その下流側の直管部4の入口部に2
枚のオリフィス9a、9bを設置することにより、短い
直管部4で大量の空気aと微量の100%濃度のアンモ
ニアガスbをアンモニア濃度のばらつきを微小に、例え
ば1%以内に収めて低濃度に混合希釈でき、直管部4が
従来の半分以下ですみコストの低減を図ることができ
る。Therefore, 100% concentration of ammonia gas b is sent in the direction opposite to the flow of the air a, the elbow 7 is installed further downstream, and the inlet 2 of the straight pipe portion 4 on the downstream side is installed.
By installing a plurality of orifices 9a and 9b, a large amount of air a and a small amount of 100% -concentration ammonia gas b can be contained in the short straight pipe portion 4 with a small dispersion of the ammonia concentration, for example, within 1% to obtain a low concentration. It is possible to mix and dilute, and the straight pipe part 4 is less than half of the conventional one, and the cost can be reduced.
【0040】図4に基づき、本発明の実施の第4形態に
かかるガス混合器を説明する。図4(a)は本実施の形
態のガス混合器14の系統図であり、同図(b)は
(a)中B部拡大断面図である。A gas mixer according to a fourth embodiment of the present invention will be described with reference to FIG. FIG. 4A is a system diagram of the gas mixer 14 of the present embodiment, and FIG. 4B is an enlarged sectional view of a B part in FIG. 4A.
【0041】図4に示すように、送風機1には送風機出
口配管2が接続されて空気aが送入され、送風機出口配
管2の途中には空気aの流れと逆向きにアンモニアガス
供給管3がその出口開口31を送風機出口配管2の上流
に向けて差し込まれて設置されている。As shown in FIG. 4, the blower outlet pipe 2 is connected to the blower 1 to feed the air a, and the ammonia gas supply pipe 3 is provided in the middle of the blower outlet pipe 2 in the direction opposite to the flow of the air a. Is installed by inserting the outlet opening 31 toward the upstream side of the blower outlet pipe 2.
【0042】アンモニアガス供給管3の位置の下流側に
はエルボ7が接続され、エルボ7の下流側には直管部4
が接続されている。そして、エルボ7の下流側の直管部
4の入口部内部に2枚のオリフィス9a、9bが一定間
隔で設置されている。An elbow 7 is connected to the downstream side of the position of the ammonia gas supply pipe 3, and a straight pipe portion 4 is connected to the downstream side of the elbow 7.
Are connected. Then, two orifices 9a and 9b are installed at regular intervals inside the inlet of the straight pipe portion 4 on the downstream side of the elbow 7.
【0043】そして前述のアンモニアガス供給管3の出
口開口31からアンモニアガス供給管3の出口開口31
の径の1倍ないし2倍の上流側位置に、出口開口31に
対面して衝突板21が設置されている。衝突板21は補
強ステー22により送風機出口配管2内に支持固定され
ている。Then, from the above-mentioned outlet opening 31 of the ammonia gas supply pipe 3 to the outlet opening 31 of the ammonia gas supply pipe 3.
A collision plate 21 is installed facing the outlet opening 31 at an upstream side position having a diameter of 1 to 2 times. The collision plate 21 is supported and fixed in the blower outlet pipe 2 by a reinforcing stay 22.
【0044】上記のようなアンモニアガス供給管3、衝
突板21、エルボ7、オリフィス9a、9bと直管部4
で構成される本実施の形態のガス混合器14において
は、送風機1からの空気aは送風機出口配管2途中の衝
突板21に衝突し、衝突板21外周に広がり流れた空気
aは衝突板21で剥離して乱れる。そこで送風機出口配
管2途中の空気aの流れと逆向きに出口開口31を向け
設置されたアンモニアガス供給管3より100%濃度の
アンモニアガスbが送入されると、アンモニアガスbは
衝突板21への衝突により衝突板21外周に広がり、乱
れた空気aの流れにより希釈されやすくなる。そしてさ
らに、エルボ7で発生する空気aの逆流域によっても混
合が促進され、直管部4入口にオリフィス9a、9bを
設置することで、1段目のオリフィス9aの絞りにより
一旦流れがせき止められアンモニアガスbの混合希釈を
促進し、更に2段目のオリフィス9bでも同様に混合希
釈を促進し、アンモニアガスbが、短い直管部4でも希
釈されやすくなる。The ammonia gas supply pipe 3, the collision plate 21, the elbow 7, the orifices 9a and 9b and the straight pipe portion 4 as described above.
In the gas mixer 14 of the present embodiment configured as described above, the air a from the blower 1 collides with the collision plate 21 in the middle of the blower outlet pipe 2, and the air a spreading and flowing to the outer periphery of the collision plate 21 collides with the collision plate 21. It peels off and is disturbed. Then, when the ammonia gas b having a 100% concentration is fed from the ammonia gas supply pipe 3 which is installed with the outlet opening 31 directed in the direction opposite to the flow of the air a in the blower outlet pipe 2, the ammonia gas b is converted into the collision plate 21. Is spread to the outer circumference of the collision plate 21 due to the collision with and is easily diluted by the turbulent flow of the air a. Further, the backflow region of the air a generated in the elbow 7 promotes the mixing, and by installing the orifices 9a and 9b at the inlet of the straight pipe portion 4, the flow is temporarily stopped by the restriction of the orifice 9a of the first stage. The mixed dilution of the ammonia gas b is promoted, and the mixed dilution is similarly promoted also in the orifice 9b of the second stage, so that the ammonia gas b is easily diluted even in the short straight pipe portion 4.
【0045】したがって、100%濃度のアンモニアガ
スbを空気aの流れと逆向きに送入し衝突板21に衝突
させ、さらに下流側にエルボ7を設置して、その下流の
直管部4入口に2枚のオリフィス9a、9bを設置する
ことにより、短い直管部4で大量の空気aと微量の10
0%濃度のアンモニアガスbをアンモニア濃度のばらつ
きを微小に、例えば1%以内に収めて低濃度に混合希釈
でき、直管部4が従来の半分以下ですみコストの低減を
図ることができる。Therefore, 100% concentration of ammonia gas b is sent in the opposite direction to the flow of the air a to collide with the collision plate 21, and further the elbow 7 is installed on the downstream side, and the inlet of the straight pipe section 4 on the downstream side. By installing two orifices 9a, 9b in the short straight pipe section 4, a large amount of air a and a small amount of 10
The ammonia gas b of 0% concentration can be mixed and diluted to a low concentration by keeping the dispersion of the ammonia concentration small, for example, within 1%, and the straight pipe portion 4 can be reduced to half or less of the conventional cost, and the cost can be reduced.
【0046】図5に基づき、本発明の実施の第5形態に
かかるガス混合器を説明する。図5は本実施の形態のガ
ス混合器15の系統図である。A gas mixer according to a fifth embodiment of the present invention will be described with reference to FIG. FIG. 5 is a system diagram of the gas mixer 15 of the present embodiment.
【0047】図5に示すように、送風機1には送風機出
口配管2が接続されて送風機1から空気aが送入され、
送風機出口配管2の下流側にはエルボ7が接続され、エ
ルボ7内の曲がり直後の内側部にアンモニアガスbを送
入する出口開口31aが開口するようにアンモニアガス
供給管3aが設置されている。エルボ7の下流側には直
管部4が接続されている。As shown in FIG. 5, the blower 1 is connected to the blower outlet pipe 2 so that the air a is fed from the blower 1.
An elbow 7 is connected to the downstream side of the blower outlet pipe 2, and an ammonia gas supply pipe 3a is installed so that an outlet opening 31a for feeding the ammonia gas b is opened inside the elbow 7 immediately after the bend. . The straight pipe portion 4 is connected to the downstream side of the elbow 7.
【0048】上記のようなエルボ7とアンモニアガス供
給管3aと直管部4で構成される本実施の形態のガス混
合器15においては、送風機1より送入される空気aは
送風機出口配管2に接続したエルボ7内の曲がり直後の
内側部で剥離し、逆流域8が比較的広範囲で生じる。エ
ルボ7の曲がりの内縁部の直後に出口開口31aが開口
するように設置されたアンモニアガス供給管3aからエ
ルボ内に送入される100%濃度のアンモニアガスb
は、逆流域8に投入され、これによりアンモニアガスb
は逆流域8で対流しながら徐々に空気aと混合し、さら
に直管部4で希釈される。In the gas mixer 15 of the present embodiment which is composed of the elbow 7, the ammonia gas supply pipe 3a and the straight pipe portion 4 as described above, the air a fed from the blower 1 is the blower outlet pipe 2 The elbow 7 connected to the inner side of the elbow 7 is separated immediately after the bend, and a backflow region 8 is generated in a relatively wide range. Ammonia gas b of 100% concentration fed into the elbow from the ammonia gas supply pipe 3a installed so that the outlet opening 31a opens immediately after the inner edge of the bend of the elbow 7.
Is fed into the reverse flow region 8 and, as a result, ammonia gas b
Is gradually mixed with air a while convection in the reverse flow region 8 and further diluted in the straight pipe portion 4.
【0049】したがって、エルボ7内の曲がりの内縁部
直後にアンモニアガス供給管3aの出口開口31aを設
置し100%濃度のアンモニアガスbを送入すること
で、短い直管部4で多量の空気aと微量の100%濃度
のアンモニアガスbをアンモニア濃度のばらつきを微小
に、例えば1%以内に収めて低濃度に混合希釈でき、直
管部4が従来の半分以下ですみコストの低減を図ること
ができる。Therefore, by providing the outlet opening 31a of the ammonia gas supply pipe 3a immediately after the inner edge of the bend in the elbow 7 and feeding the ammonia gas b having a 100% concentration, a large amount of air can be supplied to the short straight pipe portion 4. A and a small amount of 100% concentration of ammonia gas b can be mixed and diluted to a low concentration by keeping the dispersion of the ammonia concentration in a minute amount, for example, within 1%, and the straight pipe section 4 can be reduced to less than half of the conventional cost to reduce the cost. be able to.
【0050】図6に基づき、本発明の実施の第6形態に
かかるガス混合器を説明する。図6(a)は本実施の形
態のガス混合器16の系統図であり、同図(b)は、
(a)中C−C矢視断面図である。A gas mixer according to a sixth embodiment of the present invention will be described with reference to FIG. FIG. 6A is a system diagram of the gas mixer 16 of the present embodiment, and FIG.
(A) It is the CC sectional view taken on the line in the arrow.
【0051】図6に示すように、送風機1には送風機出
口配管2が接続されて送風機1から空気aが送入され、
送風機出口配管2の下流側にはエルボ7が接続され、エ
ルボ7直後の直管部4の入口部内部にディフューザ23
を設置し、ディフューザ23の絞り部(最小面積部分)
23aの外周には、アンモニアガス供給用のリングヘッ
ダ24が備えられ、リングヘッダ24にはアンモニアガ
ス供給管3bが接続されている。As shown in FIG. 6, a blower outlet pipe 2 is connected to the blower 1 so that the air a is fed from the blower 1,
An elbow 7 is connected to the downstream side of the blower outlet pipe 2, and the diffuser 23 is provided inside the straight pipe portion 4 immediately after the elbow 7.
Is installed, the throttle part of the diffuser 23 (the minimum area part)
A ring header 24 for supplying ammonia gas is provided on the outer periphery of 23a, and the ammonia gas supply pipe 3b is connected to the ring header 24.
【0052】アンモニアガス供給用のリングヘッダ24
にはディフューザ23の絞り部23aの内半径Rの約7
0%(0.7R)の長さのノズル25が、絞り部23a
の中心に向け突設され、複数、円周方向に配列して設け
られており、アンモニアガス供給管3bからのアンモニ
アガスbはノズル25から絞り部23aの中心に向け噴
出される。Ring header 24 for supplying ammonia gas
Is about 7 of the inner radius R of the throttle portion 23a of the diffuser 23.
The nozzle 25 having a length of 0% (0.7R) has a narrowed portion 23a.
A plurality of them are provided so as to project toward the center of, and are arranged in the circumferential direction, and the ammonia gas b from the ammonia gas supply pipe 3b is ejected from the nozzle 25 toward the center of the throttle portion 23a.
【0053】上記のようなエルボ7、ディフューザ2
3、リングヘッダ24、ノズル25、アンモニアガス供
給管3bと直管部4で構成される本実施の形態のガス混
合器16においては、送風機1より送入される空気a
は、エルボ7直後の直管部4入口のディフューザ23に
より、絞り部23aで空気aの流れが縮流される。この
とき、100%濃度のアンモニアガスbはアンモニアガ
ス供給管3bを介して、リングヘッダ24に供給され
る。アンモニアガスbはさらにリングヘッダ24に設け
られたノズル25から絞り部23aの中心へ絞り部23
aの内半径Rの約70%程近づいた位置で送入され、空
気aの縮流と混合し、希釈されやすくなる。Elbow 7, diffuser 2 as described above
3, the ring header 24, the nozzle 25, the ammonia gas supply pipe 3b and the straight pipe portion 4 in the gas mixer 16 of the present embodiment, the air a sent from the blower 1
The diffuser 23 at the inlet of the straight pipe portion 4 immediately after the elbow 7 reduces the flow of the air a at the throttle portion 23a. At this time, the 100% -concentration ammonia gas b is supplied to the ring header 24 via the ammonia gas supply pipe 3b. Ammonia gas b is further drawn from the nozzle 25 provided in the ring header 24 to the center of the narrowed portion 23a.
It is introduced at a position that is about 70% closer to the inner radius R of a, mixes with the contracted flow of air a, and is easily diluted.
【0054】したがって、エルボ7下流の直管部4の入
口部内部にディフューザ23を設け、その絞り部23a
の外周にアンモニアガス供給用のリングヘッダ24を設
け、リングヘッダ24に100%濃度のアンモニアガス
bが絞り部23aの中心部まで行き届くようにノズル2
5を突設することで、アンモニアガスbと絞り部23a
の空気aの縮流との混合が促進され、短い直管部4で多
量の空気aと微量の100%濃度のアンモニアガスbを
アンモニア濃度のばらつきを微小に、例えば1%以内に
収めて低濃度に混合希釈でき、直管部4が従来の半分以
下ですみコストの低減を図ることができる。Therefore, the diffuser 23 is provided inside the inlet portion of the straight pipe portion 4 downstream of the elbow 7 and the throttle portion 23a thereof is provided.
A ring header 24 for supplying ammonia gas is provided on the outer periphery of the nozzle 2 so that the ammonia gas b having a concentration of 100% reaches the center of the throttle portion 23a.
5, the ammonia gas b and the narrowed portion 23a are provided.
The mixing of the air a with the contracted flow of the air a is promoted, and a large amount of air a and a small amount of 100% concentration of the ammonia gas b are contained in the short straight pipe portion 4 with a small variation in the ammonia concentration, for example, within 1% to reduce the variation. It can be mixed and diluted to a concentration, and the straight pipe part 4 can be less than half of the conventional one, and the cost can be reduced.
【0055】図7に基づき、本発明の実施の第7形態に
かかるガス混合器を説明する。図7(a)は本実施の形
態のガス混合器17の系統図であり、同図(b)は
(a)中E部拡大断面図である。A gas mixer according to a seventh embodiment of the present invention will be described with reference to FIG. FIG. 7A is a system diagram of the gas mixer 17 of the present embodiment, and FIG. 7B is an enlarged cross-sectional view of the E portion in FIG. 7A.
【0056】図7に示すように、送風機1には送風機出
口配管2が接続されて送風機1から空気aが送入され、
送風機出口配管2の下流側にはエルボ7が接続され、エ
ルボ7の下流側には直管部4が接続している。エルボ7
の曲がり部下流側においては、エルボ7および直管部4
内の空気aの下流方向に向けて直管部4内へ延在するよ
うにアンモニアガス供給管3cが差し込まれ、アンモニ
アガス供給管3cのアンモニアガスbを空気a中に送入
する出口開口31cは空気aの下流方向に向いて開口し
ている。そして、アンモニアガス供給管3cの外周面に
は螺旋状のフィン27が設けられている。As shown in FIG. 7, a blower outlet pipe 2 is connected to the blower 1 so that air a is fed from the blower 1,
An elbow 7 is connected to the downstream side of the blower outlet pipe 2, and a straight pipe section 4 is connected to the downstream side of the elbow 7. Elbow 7
The elbow 7 and the straight pipe portion 4 are provided on the downstream side of the bent portion of
The ammonia gas supply pipe 3c is inserted so as to extend into the straight pipe portion 4 toward the downstream direction of the air a therein, and an outlet opening 31c for feeding the ammonia gas b of the ammonia gas supply pipe 3c into the air a. Is open toward the downstream side of the air a. A spiral fin 27 is provided on the outer peripheral surface of the ammonia gas supply pipe 3c.
【0057】上記のようなエルボ7、アンモニアガス供
給管3c、フィン27と直管部4で構成される本実施の
形態のガス混合器17においては、送風機1より送入さ
れた空気aは、エルボ7下流側から直管部4の上流側に
かけてアンモニアガス供給管3cのフィン27に沿って
流れ、直管部4内の上流側に旋回流27aが発生する。
この空気aの旋回流27a中にアンモニアガス供給管3
cの出口開口31cから100%濃度のアンモニアガス
bが送入されることで、アンモニアガスbが空気aと混
合希釈されやすくなり、さらに直管部4で希釈される。In the gas mixer 17 of the present embodiment which is composed of the elbow 7, the ammonia gas supply pipe 3c, the fins 27 and the straight pipe portion 4 as described above, the air a fed from the blower 1 is Flowing from the downstream side of the elbow 7 to the upstream side of the straight pipe portion 4 along the fins 27 of the ammonia gas supply pipe 3c, a swirl flow 27a is generated on the upstream side in the straight pipe portion 4.
In the swirling flow 27a of the air a, the ammonia gas supply pipe 3
When the 100% -concentration ammonia gas b is fed from the outlet opening 31c of c, the ammonia gas b is easily mixed and diluted with the air a, and is further diluted by the straight pipe portion 4.
【0058】したがって、エルボ7下流側に差し込まれ
て設置されたアンモニアガス供給管3cに螺旋状のフィ
ン27を取付けることにより、フィン27による空気a
の旋回流27aを発生させ、旋回流27a中に100%
濃度のアンモニアガスbを送入することで、アンモニア
ガスbと空気aの混合希釈が促進され、短い直管部4で
多量の空気aと微量の100%濃度のアンモニアガスb
をアンモニア濃度のばらつきを微小に、例えば1%以内
に収めて低濃度に混合希釈でき、直管部4が従来の半分
以下ですみコストの低減を図ることができる。Therefore, by attaching the spiral fin 27 to the ammonia gas supply pipe 3c which is inserted and installed on the downstream side of the elbow 7, the air
Swirl flow 27a is generated, and 100% is generated in the swirl flow 27a.
By feeding the ammonia gas b having a concentration, the mixed dilution of the ammonia gas b and the air a is promoted, and a large amount of the air a and a very small amount of the ammonia gas b having a concentration of 100% are generated in the short straight pipe portion 4.
Can be mixed and diluted to a low concentration by keeping the dispersion of the ammonia concentration minute, for example, within 1%, and the straight pipe portion 4 can be reduced to less than half that of the conventional case and the cost can be reduced.
【0059】以上、本発明の実施の形態を説明したが、
上記実施の形態に限定されるものではなく、本発明の範
囲内でその具体的構造に種々の変更を加えてもよいこと
は言うまでもない。The embodiment of the present invention has been described above.
Needless to say, the present invention is not limited to the above-described embodiment, and various modifications may be made to the specific structure within the scope of the present invention.
【0060】特に、上記従来例、実施の形態ともに空気
に100%濃度のアンモニアガスを低濃度に混合するガ
ス混合器を例に説明したが、勿論本発明は、アンモニア
に限定されるものではなく、空気に所定のガスを低濃度
に混合させるガス混合器一般に適用されるものである。In particular, both the above-mentioned conventional example and the embodiment have been described by taking a gas mixer for mixing 100% concentration of ammonia gas with air at a low concentration as an example, but the present invention is not limited to ammonia. It is generally applied to a gas mixer for mixing a predetermined gas with air at a low concentration.
【0061】[0061]
【発明の効果】(1)請求項1の発明によれば、ガス混
合器を、送風機に接続され同送風機から空気が送入され
る送風機出口配管、同送風機出口配管内にガス出口開口
を前記空気の流れの上流側に向け差し込まれて設置さ
れ、同ガス出口開口からガスを前記送風機出口配管内に
送入するガス供給管、同送風機出口配管に前記ガス供給
管の位置より下流側で接続するエルボ、同エルボの下流
側に接続する直管部を有してなるように構成したので、
ガス供給管から、ガスが空気の流れと逆向きに送入され
るとガスは空気の流れに追従されず混合が促進され希釈
されやすくなるが、さらに、空気の流れがエルボの曲が
りの内縁部で剥離を発生し逆流域が生じ、空気が乱され
ることにより、ガスの混合が促進され、短い直管部でも
希釈されやすくなり、大量の空気と微量の高濃度のガス
を濃度のばらつきを微小に、例えば1%以内に収めて低
濃度に混合希釈でき、直管部が従来の半分以下ですみコ
ストの低減を図ることができる。(1) According to the invention of claim 1, the gas mixer is provided with a blower outlet pipe connected to the blower and into which air is fed, and a gas outlet opening in the blower outlet pipe. A gas supply pipe that is installed by being inserted toward the upstream side of the air flow and that feeds gas from the gas outlet opening into the blower outlet pipe, and is connected to the blower outlet pipe downstream from the position of the gas supply pipe. Since it is configured to have an elbow and a straight pipe part connected to the downstream side of the elbow,
When the gas is introduced from the gas supply pipe in the direction opposite to the air flow, the gas does not follow the air flow, promoting mixing and facilitating dilution, but in addition, the air flow causes the elbow to bend at the inner edge. Separation causes a backflow region and disturbs the air, which promotes gas mixing and facilitates dilution even in a short straight pipe section, resulting in a large amount of air and a small amount of highly concentrated gas with uneven concentration. A small amount, for example, within 1%, can be mixed and diluted to a low concentration, and the straight pipe portion can be reduced to less than half of the conventional one, and the cost can be reduced.
【0062】(2)請求項2の発明によれば、請求項1
に記載のガス混合器において、前記直管部の入口部内部
に同直管部の中心軸回りにひねって形成されたひねり板
を取り付けてなるように構成したので、請求項1の発明
の効果に加え、空気とガスがひねり板に沿って流れ、旋
回流が発生し混合希釈を促進し、ガスが短い直管部で十
分希釈され、大量の空気と微量の高濃度のガスを濃度の
ばらつきを微小に、例えば1%以内に収めて低濃度に混
合希釈でき、直管部が従来の半分以下ですみコストの低
減を図ることができる。(2) According to the invention of claim 2, claim 1
The gas mixer according to claim 1, wherein a twist plate formed by twisting around the central axis of the straight pipe portion is attached inside the inlet portion of the straight pipe portion, and thus the effect of the invention of claim 1 In addition, air and gas flow along the twist plate, swirling flow is generated to promote mixing and dilution, the gas is sufficiently diluted in the short straight pipe part, and a large amount of air and a small amount of high concentration gas are dispersed in concentration. Can be mixed and diluted to a low concentration by containing it in a minute amount, for example, within 1%, and the straight pipe part can be reduced to less than half of the conventional cost, and the cost can be reduced.
【0063】(3)請求項3の発明によれば、請求項1
に記載のガス混合器において、前記直管部の入口部内部
にオリフィスを備えてなるように構成したので、請求項
1の発明の効果に加え、直管部の入口部にオリフィスを
設置することでオリフィスの絞りにより一旦流れがせき
止められガスの混合希釈を促進しガスが短い直管部でも
希釈されやすくなり、大量の空気と微量の高濃度のガス
を濃度のばらつきを微小に、例えば1%以内に収めて低
濃度に混合希釈でき、直管部が従来の半分以下ですみコ
ストの低減を図ることができる。
(4)請求項4の発明によれば、請求項3に記載のガス
混合器において、前記送風機出口配管内に前記ガス出口
開口に対面して取り付けられた衝突板を備えてなるよう
に構成したので、請求項3の発明の効果に加え、送風機
からの空気は送風機出口配管途中の衝突板に衝突し、衝
突板外周に広がり流れた空気は衝突板で剥離して乱れ、
ガス供給管より送入されたガスは衝突板への衝突により
衝突板外周に広がり、乱れた空気の流れにより希釈され
やすくなり、大量の空気と微量の高濃度のガスを濃度の
ばらつきを微小に、例えば1%以内に収めて低濃度に混
合希釈でき、直管部が従来の半分以下ですみコストの低
減を図ることができる。(3) According to the invention of claim 3, claim 1
In the gas mixer according to claim 1, since the orifice is provided inside the inlet portion of the straight pipe portion, in addition to the effect of the invention of claim 1, the orifice is installed at the inlet portion of the straight pipe portion. The flow is once stopped by the restriction of the orifice, which promotes the mixing and dilution of the gas, making it easier for the gas to be diluted even in a short straight pipe portion, and to make a large amount of air and a small amount of highly concentrated gas have a small concentration variation, for example, 1%. It can be mixed and diluted to a low concentration by containing it in less than half, and the straight pipe part can be reduced to less than half that of conventional products and cost can be reduced. (4) According to the invention of claim 4, in the gas mixer according to claim 3, a collision plate is installed in the blower outlet pipe so as to face the gas outlet opening. Therefore, in addition to the effect of the invention of claim 3, the air from the blower collides with the collision plate in the middle of the blower outlet pipe, and the air that has spread to the outer periphery of the collision plate is separated and disturbed by the collision plate,
The gas sent from the gas supply pipe spreads to the outer periphery of the collision plate due to the collision with the collision plate, and is easily diluted by the disturbed air flow, and a large amount of air and a small amount of highly concentrated gas have a small concentration variation. For example, it can be mixed and diluted to a low concentration by containing it within 1%, and the straight pipe part can be less than half of the conventional one, and the cost can be reduced.
【0064】(5)請求項5の発明によれば、ガス供給
管を、送風機に接続され同送風機から空気が送入される
送風機出口配管、同送風機出口配管の下流側に接続する
エルボ、同エルボの下流側に接続する直管部、前記エル
ボの曲がりの内縁部の直後にガス出口開口が開口するよ
うに設置され、同ガス出口開口からガスを前記エルボ内
に送入するガス供給管を有してなるように構成したの、
送風機より送入される空気はエルボ内の曲がりの内縁部
で剥離し、逆流域が比較的広範囲で生じ、逆流域に投入
されたガスは逆流域で対流しながら徐々に空気と混合
し、さらに直管部で希釈されるので、多量の空気と微量
の高濃度のガスを濃度のばらつきを微小に、例えば1%
以内に収めて低濃度に混合希釈でき、直管部が従来の半
分以下ですみコストの低減を図ることができる。(5) According to the invention of claim 5, the gas supply pipe is connected to the blower, the blower outlet pipe to which air is fed from the blower, the elbow connected to the downstream side of the blower outlet pipe, and the same. A straight pipe part connected to the downstream side of the elbow, a gas outlet opening is installed immediately after the inner edge of the bend of the elbow, and a gas supply pipe for introducing gas into the elbow from the gas outlet opening is provided. I configured it to have,
The air blown from the blower separates at the inner edge of the bend in the elbow, and a backflow region occurs in a relatively wide range.The gas injected into the backflow region gradually convects in the backflow region and gradually mixes with the air. Since it is diluted in the straight pipe section, a large amount of air and a small amount of high-concentration gas can be used, for example, with a small concentration variation, for example, 1%.
It can be mixed and diluted to a low concentration by containing it in less than half, and the straight pipe part can be reduced to less than half that of conventional products and cost can be reduced.
【0065】(6)請求項6の発明によれば、ガス供給
管を、送風機に接続され同送風機から空気が送入される
送風機出口配管、同送風機出口配管の下流側に接続する
エルボ、同エルボの下流側に接続する直管部、同直管部
の入口部内部に形成されたディフューザ、同ディフュー
ザの絞り部の外周に備えられたリングヘッダ、同リング
ヘッダに連通して設置されたガス供給管、同リングヘッ
ダに前記絞り部の中心に向け突設され前記ガス供給管か
ら供給されたガスを前記絞り部内に送入する複数のノズ
ルを有してなるように構成したので、送風機より送入さ
れる空気はディフューザにより絞り部で縮流され、ガス
供給管を介してリングヘッダに供給されたガスはノズル
から絞り部の中心近くに送入され空気の縮流と混合し、
希釈されやすくなり、短い直管部で多量の空気と微量の
高濃度のガスを濃度のばらつきを微小に、例えば1%以
内に収めて低濃度に混合希釈でき、直管部が従来の半分
以下ですみコストの低減を図ることができる。(6) According to the invention of claim 6, the gas supply pipe is connected to a blower, and a blower outlet pipe is connected to the blower for feeding air, and an elbow connected to the downstream side of the blower outlet pipe. A straight pipe part connected to the downstream side of the elbow, a diffuser formed inside the inlet part of the straight pipe part, a ring header provided on the outer periphery of the throttle part of the diffuser, and a gas installed in communication with the ring header Since the supply pipe and the ring header are provided with a plurality of nozzles projecting toward the center of the throttle portion and for feeding the gas supplied from the gas supply pipe into the throttle portion, The air sent in is contracted by the diffuser at the throttle part, and the gas supplied to the ring header via the gas supply pipe is sent from the nozzle near the center of the throttle part and mixed with the contracted flow of air,
It becomes easy to dilute, and it is possible to mix and dilute a large amount of air and a small amount of high-concentration gas in a short straight pipe part with a small concentration variation, for example within 1% to a low concentration, and the straight pipe part is less than half of the conventional Therefore, the cost can be reduced.
【0066】(7)請求項7の発明によれば、ガス供給
管を、送風機に接続され同送風機から空気が送入される
送風機出口配管、同送風機出口配管の下流側に接続する
エルボ、同エルボの下流側に接続する直管部、同エルボ
内の下流側において前記空気の流れの下流方向に向いて
前記直管部内に延在するように差し込まれて設置されガ
ス出口開口が同空気の流れの下流方向に向けて開口し同
ガス出口開口から前記直管部内にガスを送入するガス供
給管、同ガス供給管の外周に取り付けられた螺旋状のフ
ィンを有してなるように構成したので、送風機より送入
された空気は、ガス供給管の外周の螺旋状のフィンに沿
って流れ、発生した旋回流中にガス供給管から送入され
たガスが空気と混合希釈されやすくなり、短い直管部で
多量の空気と微量の高濃度のガスを濃度のばらつきを微
小に、例えば1%以内に収めて低濃度に混合希釈でき、
直管部が従来の半分以下ですみコストの低減を図ること
ができる。(7) According to the invention of claim 7, the gas supply pipe is connected to the blower, the blower outlet pipe to which air is fed from the blower, the elbow connected to the downstream side of the blower outlet pipe, The straight pipe portion connected to the downstream side of the elbow, the gas outlet opening is installed so as to extend in the straight pipe portion toward the downstream direction of the air flow on the downstream side in the elbow A gas supply pipe that opens in the downstream direction of the flow and that feeds gas into the straight pipe portion from the gas outlet opening, and a spiral fin attached to the outer circumference of the gas supply pipe Therefore, the air sent from the blower flows along the spiral fins on the outer circumference of the gas supply pipe, and the gas sent from the gas supply pipe is easily mixed and diluted with air during the generated swirling flow. , Short straight pipe section with a large amount of air and trace amount The high concentration of gas in small variations in concentration, for example, can be mixed and diluted to a low concentration contained within 1%,
Since the straight pipe section is less than half that of the conventional type, the cost can be reduced.
【図1】本発明の実施の第1形態にかかるガス混合器の
系統図である。FIG. 1 is a system diagram of a gas mixer according to a first embodiment of the present invention.
【図2】(a)は本発明の実施の第2形態にかかるガス
混合器の系統図であり、(b)は(a)中A部拡大断面
図である。FIG. 2 (a) is a system diagram of a gas mixer according to a second embodiment of the present invention, and FIG. 2 (b) is an enlarged cross-sectional view of a portion A in (a).
【図3】本発明の実施の第3形態にかかるガス混合器の
系統図である。FIG. 3 is a system diagram of a gas mixer according to a third embodiment of the present invention.
【図4】(a)は本発明の実施の第4形態にかかるガス
混合器の系統図であり、(b)は(a)中B部拡大断面
図である。FIG. 4 (a) is a system diagram of a gas mixer according to a fourth embodiment of the present invention, and FIG. 4 (b) is an enlarged cross-sectional view of portion B in (a).
【図5】本発明の実施の第5形態にかかるガス混合器の
系統図である。FIG. 5 is a system diagram of a gas mixer according to a fifth embodiment of the present invention.
【図6】(a)は本発明の実施の第6形態にかかるガス
混合器の系統図であり、(b)は、(a)中C−C矢視
断面図である。FIG. 6 (a) is a system diagram of a gas mixer according to a sixth embodiment of the present invention, and FIG. 6 (b) is a sectional view taken along line CC in FIG. 6 (a).
【図7】(a)は本発明の実施の第7形態にかかるガス
混合器の系統図であり、(b)は(a)中E部拡大断面
図である。FIG. 7 (a) is a system diagram of a gas mixer according to a seventh embodiment of the present invention, and FIG. 7 (b) is an enlarged cross-sectional view of an E section in (a).
【図8】従来のガス混合器の系統図である。FIG. 8 is a system diagram of a conventional gas mixer.
1 送風機
2 送風機出口配管
3、3a、3b、3c アンモニアガス供給管
4 直管部
5 ダクト
6 アンモニアガス注入ノズ
ル
7 エルボ
8 逆流部
9a、9b オリフィス
11、12、13、14、15、16、17
ガス混合器
21 衝突板
22 補強ステー
23 ディフューザ
23a 絞り部
24 リングヘッダ
25 ノズル
26 ひねり板
26a 旋回流
27 フィン
27a 旋回流
31、31a、31c 出口開口1 Blower 2 Blower outlet pipe 3, 3a, 3b, 3c Ammonia gas supply pipe 4 Straight pipe portion 5 Duct 6 Ammonia gas injection nozzle 7 Elbow 8 Backflow portion 9a, 9b Orifice 11, 12, 13, 14, 15, 16, 17 Gas mixer 21 Collision plate 22 Reinforcing stay 23 Diffuser 23a Throttle portion 24 Ring header 25 Nozzle 26 Twist plate 26a Swirling flow 27 Fin 27a Swirling flow 31, 31a, 31c Exit opening
フロントページの続き (72)発明者 谷口 雅章 長崎市深堀町五丁目717番1号 三菱重工 業株式会社長崎研究所内 (72)発明者 浦田 信也 長崎市深堀町五丁目717番1号 三菱重工 業株式会社長崎研究所内 Fターム(参考) 4D002 AA12 BA06 CA01 DA07 GA03 GB20 4G035 AB02 AC06 AC10 AC12 Continued front page (72) Inventor Masaaki Taniguchi 5-717-1, Fukahori-cho, Nagasaki-shi Mitsubishi Heavy Industries Business Nagasaki Institute (72) Inventor Shinya Urata 5-717-1, Fukahori-cho, Nagasaki-shi Mitsubishi Heavy Industries Business Nagasaki Institute F-term (reference) 4D002 AA12 BA06 CA01 DA07 GA03 GB20 4G035 AB02 AC06 AC10 AC12
Claims (7)
される送風機出口配管、同送風機出口配管内にガス出口
開口を前記空気の流れの上流側に向け差し込まれて設置
され、同ガス出口開口からガスを前記送風機出口配管内
に送入するガス供給管、同送風機出口配管に前記ガス供
給管の位置より下流側で接続するエルボ、同エルボの下
流側に接続する直管部を有してなることを特徴とするガ
ス混合器。1. A blower outlet pipe connected to a blower for feeding air from the blower, and a gas outlet opening is inserted into the blower outlet pipe so as to be directed toward an upstream side of the air flow. It has a gas supply pipe for feeding gas from the opening into the blower outlet pipe, an elbow connected to the blower outlet pipe downstream of the position of the gas supply pipe, and a straight pipe portion connected to the downstream side of the elbow. A gas mixer characterized in that
記直管部の入口部内部に同直管部の中心軸回りにひねっ
て形成されたひねり板を取り付けてなることを特徴とす
るガス混合器。2. The gas mixer according to claim 1, wherein a twist plate formed by twisting around the central axis of the straight pipe portion is attached inside the inlet portion of the straight pipe portion. Gas mixer.
記直管部の入口部内部にオリフィスを備えてなることを
特徴とするガス混合器。3. The gas mixer according to claim 1, wherein an orifice is provided inside the inlet of the straight pipe section.
記送風機出口配管内に前記ガス出口開口に対面して取り
付けられた衝突板を備えてなることを特徴とするガス混
合器。4. The gas mixer according to claim 3, further comprising: a collision plate mounted inside the blower outlet pipe so as to face the gas outlet opening.
される送風機出口配管、同送風機出口配管の下流側に接
続するエルボ、同エルボの下流側に接続する直管部、前
記エルボの曲がりの内縁部の直後にガス出口開口が開口
するように設置され、同ガス出口開口からガスを前記エ
ルボ内に送入するガス供給管を有してなることを特徴と
するガス混合器。5. A blower outlet pipe connected to a blower and receiving air from the blower, an elbow connected to the downstream side of the blower outlet pipe, a straight pipe portion connected to the downstream side of the elbow, and a bend of the elbow. A gas mixer, which is installed so that a gas outlet opening is opened immediately after the inner edge of the gas mixer, and has a gas supply pipe for feeding gas into the elbow from the gas outlet opening.
される送風機出口配管、同送風機出口配管の下流側に接
続するエルボ、同エルボの下流側に接続する直管部、同
直管部の入口部内部に形成されたディフューザ、同ディ
フューザの絞り部の外周に備えられたリングヘッダ、同
リングヘッダに連通して設置されたガス供給管、同リン
グヘッダに前記絞り部の中心に向け突設され前記ガス供
給管から供給されたガスを前記絞り部内に送入する複数
のノズルを有してなることを特徴とするガス混合器。6. A blower outlet pipe connected to a blower and receiving air from the blower, an elbow connected to the downstream side of the blower outlet pipe, a straight pipe portion connected to the downstream side of the elbow, and a straight pipe portion. Formed inside the inlet of the diffuser, a ring header provided on the outer periphery of the throttle part of the diffuser, a gas supply pipe installed in communication with the ring header, and a protrusion on the ring header toward the center of the throttle part A gas mixer, comprising a plurality of nozzles that are provided and that feed the gas supplied from the gas supply pipe into the narrowed portion.
される送風機出口配管、同送風機出口配管の下流側に接
続するエルボ、同エルボの下流側に接続する直管部、同
エルボ内の下流側において前記空気の流れの下流方向に
向いて前記直管部内に延在するように差し込まれて設置
されガス出口開口が同空気の流れの下流方向に向けて開
口し同ガス出口開口から前記直管部内にガスを送入する
ガス供給管、同ガス供給管の外周に取り付けられた螺旋
状のフィンを有してなることを特徴とするガス混合器。7. A blower outlet pipe connected to a blower for feeding air from the blower, an elbow connected to the downstream side of the blower outlet pipe, a straight pipe portion connected to the downstream side of the blower, and the inside of the elbow. On the downstream side, the gas outlet opening is installed to be inserted so as to extend in the straight pipe portion toward the downstream direction of the air flow, and the gas outlet opening is opened toward the downstream direction of the air flow and from the gas outlet opening. A gas mixer comprising: a gas supply pipe for feeding gas into a straight pipe portion; and a spiral fin attached to the outer periphery of the gas supply pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001320547A JP2003117367A (en) | 2001-10-18 | 2001-10-18 | Gas mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001320547A JP2003117367A (en) | 2001-10-18 | 2001-10-18 | Gas mixer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2003117367A true JP2003117367A (en) | 2003-04-22 |
Family
ID=19137922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2001320547A Withdrawn JP2003117367A (en) | 2001-10-18 | 2001-10-18 | Gas mixer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2003117367A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006326571A (en) * | 2005-04-28 | 2006-12-07 | Hitachi Ltd | Fluid mixing device |
| JP2009521317A (en) * | 2005-12-23 | 2009-06-04 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | Controlled combustion for regenerative reactor with mixer / flow distributor |
| JP2010280808A (en) * | 2009-06-04 | 2010-12-16 | Jfe Steel Corp | Coke oven fuel gas mixing device |
| KR20150057573A (en) * | 2013-11-20 | 2015-05-28 | 이향천 | Large size combustion instrument for cooking |
| CN108722184A (en) * | 2017-12-22 | 2018-11-02 | 上海明华电力技术工程有限公司 | A kind of accurate spray ammonia system of the adaptive leveling of full load |
| KR102497075B1 (en) * | 2022-08-16 | 2023-02-07 | 삼동환경(주) | PH reducing apparatus of waste water using carbondioxide gas |
| JP2023523563A (en) * | 2020-04-16 | 2023-06-06 | エドワーズ リミテッド | Dilution of combustible gas |
-
2001
- 2001-10-18 JP JP2001320547A patent/JP2003117367A/en not_active Withdrawn
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006326571A (en) * | 2005-04-28 | 2006-12-07 | Hitachi Ltd | Fluid mixing device |
| JP2009521317A (en) * | 2005-12-23 | 2009-06-04 | エクソンモービル リサーチ アンド エンジニアリング カンパニー | Controlled combustion for regenerative reactor with mixer / flow distributor |
| JP2010280808A (en) * | 2009-06-04 | 2010-12-16 | Jfe Steel Corp | Coke oven fuel gas mixing device |
| KR20150057573A (en) * | 2013-11-20 | 2015-05-28 | 이향천 | Large size combustion instrument for cooking |
| KR101579152B1 (en) * | 2013-11-20 | 2015-12-22 | 이향천 | Large size combustion instrument for cooking |
| CN108722184A (en) * | 2017-12-22 | 2018-11-02 | 上海明华电力技术工程有限公司 | A kind of accurate spray ammonia system of the adaptive leveling of full load |
| CN108722184B (en) * | 2017-12-22 | 2024-09-03 | 上海明华电力科技有限公司 | Full-load self-adaptive leveling accurate ammonia spraying system |
| JP2023523563A (en) * | 2020-04-16 | 2023-06-06 | エドワーズ リミテッド | Dilution of combustible gas |
| JP7685521B2 (en) | 2020-04-16 | 2025-05-29 | エドワーズ リミテッド | Dilution of flammable gases |
| US12397270B2 (en) | 2020-04-16 | 2025-08-26 | Edwards Limited | Flammable gas dilution |
| KR102497075B1 (en) * | 2022-08-16 | 2023-02-07 | 삼동환경(주) | PH reducing apparatus of waste water using carbondioxide gas |
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Legal Events
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| A300 | Application deemed to be withdrawn because no request for examination was validly filed |
Free format text: JAPANESE INTERMEDIATE CODE: A300 Effective date: 20050104 |